JPH0649790B2 - Opaque stretched molded article and method for producing the same - Google Patents
Opaque stretched molded article and method for producing the sameInfo
- Publication number
- JPH0649790B2 JPH0649790B2 JP2001053A JP105390A JPH0649790B2 JP H0649790 B2 JPH0649790 B2 JP H0649790B2 JP 2001053 A JP2001053 A JP 2001053A JP 105390 A JP105390 A JP 105390A JP H0649790 B2 JPH0649790 B2 JP H0649790B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- parts
- petroleum resin
- softening point
- cyclopentadiene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Moulding By Coating Moulds (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ポリプロピレン系樹脂を主成分とする延伸成
形物に関する。さらに詳しくは結晶性ポリプロピレンに
特定の石油系炭化水素樹脂および無機充填剤を添加した
組成物を延伸して、成形物内部ないしは表面に微細な空
洞を多数発生させ、不透明感ないしはパール感を付与し
た延伸成形物及びその製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of use] The present invention relates to a stretch-molded article containing a polypropylene resin as a main component. More specifically, a composition obtained by adding a specific petroleum hydrocarbon resin and an inorganic filler to crystalline polypropylene was stretched to generate a large number of fine voids inside or on the surface of the molded article, and imparted with an opaque or pearly feeling. The present invention relates to a stretched molded product and a method for producing the same.
一般に、パール感ないし不透明感を有する成形物は、例
えば、一軸ないし二軸延伸フィルムとして一般包装材
料、装飾材料、合成紙または書写印刷紙等に用いられ、
又、テープ、リボンまたはフィラメントとして梱包材
料、織糸等に広く用いられている。Generally, a molded article having a pearly feeling or an opaque feeling is used, for example, as a uniaxially or biaxially stretched film in general packaging materials, decorative materials, synthetic papers, calligraphic printing papers, and the like.
It is also widely used as a tape, ribbon or filament for packing materials, woven yarns and the like.
従来、成形物をパール化ないし不透明化する方法として
は、(1)白色顔料、体質顔料あるいはパールエッセンス
等の光沢物質を添加する方法、(2)成形時に発泡剤を添
加して多数の気泡を形成させる方法、(3)特開昭63−24
532号公報、特開昭63−117043号公報等に記載されるご
とく無機充填剤を多量に添加した後、延伸しボイドを形
成させる方法、(4)成形物を溶剤あるいは薬品等で処理
してダル化させる方法、(5)ナイロン、ポリエステル等
高融点ポリマーをポリプロピレンに分散させる方法(米
国特許第4,377,616 号、特開昭61−157547号公報)が知
られている。Conventionally, as a method for making a molded article pearlized or opaque, (1) a method of adding a glossy substance such as a white pigment, an extender pigment or pearl essence, (2) a foaming agent is added at the time of molding to generate a large number of bubbles. Forming method, (3) JP-A-63-24
A method of adding a large amount of an inorganic filler as described in JP-A No. 532, JP-A-63-117043, and the like, followed by stretching to form voids. (4) Treating the molded product with a solvent or chemicals A method of dulling and (5) a method of dispersing a high melting point polymer such as nylon and polyester in polypropylene (U.S. Pat. No. 4,377,616, JP-A-61-157547) are known.
しかし、これらの方法は、次のような欠点を有する。す
なわち、(1)については不透明化、パール化で顔料を使
い分ける必要があり、パールエッセンスは、また非常に
高価である。更に、これら顔料の分散に特に考慮した混
合方法および装置を要する。(2)については成形条件、
用途による発泡剤の選択が必要であり、フィルム等の薄
膜では均一な微細発泡が得難いという欠点を有する。However, these methods have the following drawbacks. That is, regarding (1), it is necessary to use different pigments for opacification and pearlization, and pearl essence is also very expensive. In addition, a mixing method and apparatus that take into consideration the dispersion of these pigments are required. For (2), molding conditions,
It is necessary to select a foaming agent depending on the application, and it is difficult to obtain uniform fine foaming with a thin film such as a film.
(3)については、無機充填剤を多量に添加する事により
不透明化はし易いが、押出時の流動性が大幅に低下した
り、スクリーンパックが目詰まりしたり、無機充填剤に
起因する吸湿・発泡や分散不良を生じ易く、樹脂の置換
にも長時間を要する等の生産時のトラブルが多い、得ら
れた製品も光沢度が低下したり、表面が粗面化したもの
しか得られない。また耐衝撃性が劣る等の欠点がある。
また(4)は、後処理工程で行われ、かつ、溶剤・薬品類
の除去工程も必要で、装置、経費の面で不利であり、ま
た製品もダル感は得られるがパール感を有する製品は得
られないという問題がある。また(5)のポリプロピレン
にナイロン、ポリエステル等の不相溶性ポリマーを添加
した配合物を、延伸し、不透明化する方法(米国特許第
4,377,616号)は、ナイロン、ポリエステルはポリプロ
ピレンとの相溶性に劣り、流動性もきわめて異なるため
に均一分散が困難であり、安定生産性に劣り、均一な不
透明フィルムを安定して得難いという問題がある。Regarding (3), it is easy to make opaque by adding a large amount of inorganic filler, but the fluidity during extrusion is significantly reduced, the screen pack is clogged, and moisture absorption due to the inorganic filler is caused.・ There are many troubles during production, such as foaming and poor dispersion, and it takes a long time to replace the resin. Only the product obtained has a reduced glossiness or a roughened surface. . Further, there are drawbacks such as poor impact resistance.
In addition, (4) is performed in a post-treatment process and requires a process for removing solvents and chemicals, which is disadvantageous in terms of equipment and cost. Also, the product has a pearly feeling although a dull feeling is obtained. There is a problem that can not be obtained. In addition, a method of stretching a compound obtained by adding an incompatible polymer such as nylon or polyester to polypropylene of (5) to make it opaque (US Patent No.
No. 4,377,616) nylon and polyester have poor compatibility with polypropylene and have very different fluidity, making uniform dispersion difficult, resulting in poor stable productivity and difficulty in obtaining a uniform opaque film in a stable manner. .
本発明の目的は、前記従来の不透明化フィルムの問題点
を解決し、改良された不透明感、パール感を有し、軽量
でガスバリヤー性も良好であり、少量の無機充填剤の配
合で不透明化が達成でき、生産時のトラブル、装置、経
費の面での不利な点もなく、安定生産性に少れた均一な
不透明フィルム及びその製造方法を提供することであ
る。The object of the present invention is to solve the problems of the conventional opacifying film, to have an improved opacity and pearly feeling, to be lightweight and to have good gas barrier properties, and to be opaque by blending a small amount of an inorganic filler. The object of the present invention is to provide a uniform opaque film with less stable productivity and a method for producing the same, which is capable of achieving high efficiency, has no disadvantages in terms of production troubles, equipment and costs.
本発明者らは、不透明化に最も有用な上記(3)の方法の
生産性および製品の光沢改良について、種々検討した結
果、特定の軟化点を有するシクロペンタジエン系石油樹
脂と無機充填剤を併用添加した組成物を用いる事によっ
て、ポリプロピレンに無機充填剤のみを配合した組成物
を用いた場合よりも、改良された不透明感・パール感等
を有し、かつ、軽量で、ガスバリヤー性も良好な成形品
が得られ、かつ、少量の無機充填剤の配合で不透明化が
達成出来、きわめて生産性も優れる事を知見し、本発明
に到達した。As a result of various studies on the productivity of the method (3) most useful for opacification and the gloss improvement of the product, the present inventors have used a cyclopentadiene-based petroleum resin having a specific softening point and an inorganic filler in combination. By using the added composition, it has improved opacity, pearly feeling, etc., and is lighter and has better gas barrier properties than the case of using a composition in which only an inorganic filler is mixed with polypropylene. The present inventors have found that various molded products can be obtained, opacity can be achieved by adding a small amount of an inorganic filler, and productivity is extremely excellent, and the present invention has been achieved.
すなわち本発明は、 (1) 結晶性ポリプロピレン100重量部に対し、無
機充填剤粉末0.1〜20重量部および軟化点(環球
法)160℃以上のシクロペンタジエン系石油樹脂3〜
40重量部を配合した組成物からなり、微細な空洞を多
数有して、その全光線透過率が50%以下、密度が0.
8g/cm3以下である不透明化した延伸成形物、 (2) 結晶性ポリプロピレン100重量部に対し、無
機充填剤粉末0.1〜20重量部および軟化点(環球
法)160℃以上の水素化シクロペンタジエン系石油樹
脂3〜40重量部を配合した組成物を、該結晶性ポリプ
ロピレンの結晶融点及び該石油樹脂の軟化点より10℃
以上高い温度で溶融押出し、冷却して未延伸原反を作製
した後、該ポリプロピレンの融点及び該石油樹脂の軟化
点より低い温度で、少なくとも一方向に2倍以上延伸
し、微細な空洞を多数発生させることを特徴とする不透
明化した延伸成形物の製造方法、 (3) シクロペンタジエン成分を50重量%以上含有
する石油樹脂を水素化して得られた軟化点(環球法)1
70〜200℃、ヨウ素価20以下の水素化シクロペン
タジエン系石油樹脂を用いた前記(1)記載の不透明化
した延伸成形物、 (4) シクロペンタジエン成分を50重量%以上含有
する石油樹脂を水素化して得られた軟化点(環球法)1
70〜200℃、ヨウ素価20以下の水素化シクロペン
タジエン系石油樹脂を用いることを特徴とする前記
(2)記載の不透明化した延伸成形物の製造方法。That is, the present invention includes: (1) 0.1 to 20 parts by weight of an inorganic filler powder and 100 to 100 parts by weight of crystalline polypropylene, and a cyclopentadiene-based petroleum resin 3 having a softening point (ring and ball method) of 160 ° C. or higher.
It is composed of a composition containing 40 parts by weight, has a large number of fine cavities, and has a total light transmittance of 50% or less and a density of 0.
An opaque stretch-molded product having a weight of 8 g / cm 3 or less, (2) 0.1 to 20 parts by weight of inorganic filler powder and hydrogenation at a softening point (ring and ball method) of 160 ° C. or more based on 100 parts by weight of crystalline polypropylene. A composition prepared by blending 3 to 40 parts by weight of a cyclopentadiene-based petroleum resin was prepared at 10 ° C from the crystalline melting point of the crystalline polypropylene and the softening point of the petroleum resin.
After melt-extruding at a higher temperature and cooling to prepare an unstretched raw fabric, it is stretched at least twice in at least one direction at a temperature lower than the melting point of the polypropylene and the softening point of the petroleum resin to form many fine cavities. (3) Softening point (ring and ball method) obtained by hydrogenating a petroleum resin containing 50% by weight or more of a cyclopentadiene component.
An opaque stretched molded article according to (1) above, which uses a hydrogenated cyclopentadiene-based petroleum resin having a iodine value of 20 or less at 70 to 200 ° C. (4) Hydrogen petroleum resin containing 50% by weight or more of a cyclopentadiene component Softening point (ring and ball method) 1
The method for producing an opaque stretched molded article according to (2) above, which comprises using a hydrogenated cyclopentadiene-based petroleum resin having a iodine value of 20 or less at 70 to 200 ° C.
(5) 無機充填剤として、平均粒径が10μ以下の炭
酸カルシウムまたは/およびタルクを1〜10重量部配
合した組成物を用いる事を特徴とする前記(2)記載の
不透明化した延伸成形物の製造方法、 (6) 無機充填剤として、平均粒径が10μ以下のシ
リカまたは/および珪酸塩0.1〜2.0重量部を配合
した組成物を用いる事を特徴とする前記(2)記載の不
透明化した延伸成形物の製造方法、 に関するものである。(5) An opaque stretched molded article according to the above (2), characterized in that a composition containing 1 to 10 parts by weight of calcium carbonate or / and talc having an average particle diameter of 10 μm or less is used as the inorganic filler. (6) A composition containing 0.1 to 2.0 parts by weight of silica or / and a silicate having an average particle size of 10 μ or less is used as the inorganic filler, (2) The present invention relates to the method for producing an opaque stretch-molded product described above.
本発明で用いられる結晶性ポリプロピレンは、プロピレ
ンの単独重合体、プロピレンを主成分とするエチレン又
は/及び他のα−オレフィンとの共重合体、またはそれ
らの混合物である。The crystalline polypropylene used in the present invention is a homopolymer of propylene, a copolymer containing propylene as a main component with ethylene or / and another α-olefin, or a mixture thereof.
本発明で用いる無機充填剤は、炭酸カルシウム、タル
ク、クレー、カオリン、シリカ、珪藻土、炭酸マグネシ
ウム、炭酸バリウム、硫酸マグネシウム、硫酸バリウ
ム、硫酸カルシウム、水酸化アルミニウム、水酸化マグ
ネシウム、アルミナ、マイカ、ガラス粉、シラスバルー
ン、ゼオライト、ハイドロタルサイト、酸化チタン、酸
化アルミニウム等の金属の酸化物等ポリオレフィンの延
伸加工による多孔化に用いる事が公知の各種無機充填剤
を用いる事が出来、このうち、平均粒径が10μ以下の
炭酸カルシウム、タルク、クレー、シリカまたは珪酸塩
等が特に好ましい。この平均粒径が大きすぎると、製造
時にトラブルを発生し易く、得られた製品も、粗面化
し、表面光沢が著しく低下する。The inorganic filler used in the present invention is calcium carbonate, talc, clay, kaolin, silica, diatomaceous earth, magnesium carbonate, barium carbonate, magnesium sulfate, barium sulfate, calcium sulfate, aluminum hydroxide, magnesium hydroxide, alumina, mica, glass. Powders, shirasu balloons, zeolites, hydrotalcites, titanium oxides, oxides of metals such as aluminum oxide, and the like can be used various inorganic fillers known to be used for porosification of polyolefins by stretching, and among them, the average Calcium carbonate, talc, clay, silica or silicate having a particle size of 10 μm or less is particularly preferable. If this average particle size is too large, troubles are likely to occur during production, and the obtained product also has a roughened surface and the surface gloss is significantly reduced.
なお、これら無機充填剤を数種混合使用しても良い。ま
た、これらの充填剤を脂肪酸またはその金属塩、シラン
カップリング剤等公知のもので表面処理したものを用い
る事も出来る。In addition, you may use these inorganic fillers in mixture of several types. Further, it is also possible to use those obtained by surface-treating these fillers with known substances such as fatty acids or metal salts thereof, silane coupling agents and the like.
本発明で用いるシクロペンタジエン系石油樹脂は、石油
ナフサなどのスチームクラッキングなどから得られるシ
クロペンタジエン、ジシクロペンタジエンおよびその多
量体あるいはそれらのアルキル置換体あるいはそれらの
混合物等を主成分とする留分を溶剤の存在下または不存
在下に、窒素ガス等の不活性ガスの雰囲気下で、好まし
くは220〜320℃の温度で、重合系を液相に保持し
得る以上の圧力下で、数時間以上熱重合して得たシクロ
ペンタジエン系成分を50重量%以上含有する高分子量
・高軟化点シクロペンタジエン系石油樹脂、及び該石油
樹脂を従来公知の方法、すなわち、パラジウム、ニッケ
ル、コバルト等の金属またはその酸化物等の触媒を用
い、溶剤の存在下150〜300℃の温度、10〜15
0kg/cm2の水素圧の条件下で水素化した水素化シクロ
ペンタジエン系石油樹脂またはそれらの混合物である。
このシクロペンタジエン留分の重合は、一段でも良い
が、例えばジシクロペンタジエンを二段階に重合させる
等の二段以上で重合するのも良く、重合工程、重合及び
水素化工程は連続式あるいはバッチ式のいずれでも良
い。The cyclopentadiene-based petroleum resin used in the present invention is a cyclopentadiene obtained from steam cracking of petroleum naphtha or the like, dicyclopentadiene and a multimer thereof or an alkyl-substituted fraction thereof or a mixture thereof as a main component. In the presence or absence of a solvent, under an atmosphere of an inert gas such as nitrogen gas, preferably at a temperature of 220 to 320 ° C., under a pressure at which the polymerization system can be maintained in a liquid phase, for several hours or more. A high molecular weight / high softening point cyclopentadiene-based petroleum resin containing 50 wt% or more of a cyclopentadiene-based component obtained by thermal polymerization, and a conventionally known method for producing the petroleum resin, that is, a metal such as palladium, nickel or cobalt, or Using a catalyst such as the oxide, in the presence of a solvent, a temperature of 150 to 300 ° C., a temperature of 10 to 15
It is a hydrogenated cyclopentadiene-based petroleum resin or a mixture thereof hydrogenated under a hydrogen pressure of 0 kg / cm 2 .
The cyclopentadiene fraction may be polymerized in one step, but it may be polymerized in two or more steps, for example, dicyclopentadiene is polymerized in two steps. The polymerization step, the polymerization and the hydrogenation step may be continuous or batch type. Any of
こうして得られたシクロペンタジエン系石油樹脂のう
ち、本発明においては、その軟化点(環球法)が160
℃以上のものでなければならない。軟化点が160℃に
達しないものは不透明感・パール感共に不足し、本発明
の目的とする延伸成形物は得られず150℃以下では、
特開昭61−203140号公報や、従来公知の水素化石油樹脂
と同様に、本発明とまったく逆の方向、すなわち成形物
が透明化し、本発明の目的とする不透明で、微細な空洞
を含有し、パール光沢を有する等のきわめて特徴的な延
伸成形品を得る事は出来ない。Among the cyclopentadiene-based petroleum resins thus obtained, their softening point (ring and ball method) is 160 in the present invention.
Must be above ℃. If the softening point does not reach 160 ° C, both the opaqueness and the pearly feeling are insufficient, and the stretch-molded article aimed at by the present invention cannot be obtained.
As in JP-A-61-203140 and conventionally known hydrogenated petroleum resins, the direction is completely opposite to that of the present invention, that is, the molded product is transparent and contains opaque and minute cavities for the purpose of the present invention. However, it is impossible to obtain a stretch-molded product having a very characteristic property such as having a pearly luster.
本発明においては、軟化点が160℃以上の水素化シク
ロペンタジエン系石油樹脂が好ましく、軟化点170〜
200℃で、かつ、ゲルパーミーエーションクロマトグ
ラフィー法で測定した平均分子量が1200以上、ヨウ
素価20以下の水素化シクロペンタジエン系石油樹脂
が、ポリプロピレンとの相溶性に優れ、無機充填剤との
分散性も良好で、安定して加工が出来、かつ、白色度・
不透明感の優れた延伸成形物が得られ、特に好ましい。
この水素化シクロペンタジエン系樹脂は、ナイロン、飽
和ポリエステル系樹脂等の高融点ポリマーに比して、結
晶性ポリプロピレンとの相溶性に優れ均一分散が可能で
あり、原反成形性、延伸性等生産性に優れ、かつ、得ら
れた成形物も高光沢で、均一な製品が得られる。In the present invention, a hydrogenated cyclopentadiene-based petroleum resin having a softening point of 160 ° C. or higher is preferable, and a softening point of 170 to
Hydrogenated cyclopentadiene-based petroleum resin having an average molecular weight of 1200 or more and an iodine value of 20 or less measured at 200 ° C. by a gel permeation chromatography method has excellent compatibility with polypropylene and dispersibility with an inorganic filler. Also good, stable processing, and whiteness
A stretched molded article having excellent opacity is obtained, which is particularly preferable.
Compared with high melting point polymers such as nylon and saturated polyester resins, this hydrogenated cyclopentadiene resin has excellent compatibility with crystalline polypropylene and can be uniformly dispersed. A molded product having excellent properties and a high gloss is obtained, and a uniform product can be obtained.
本発明で用いる組成物は、ポリプロピレン100重量部
に対し、無機充填剤粉末0.1〜20重量部および軟化
点(環球法)160℃以上のシクロペンタジエン系石油
樹脂を3〜40重量部配合する。無機充填剤の添加量が
0.1重量部未満では光線透過率が大きく不透明度が不
足し、20重量部を越えるとフィルム製造時に目詰ま
り、分散不良および延伸切れ等のトラブルを発生し易
く、得られたフィルムも表面光沢が低下し、パール感が
低下するので好ましくない。また、該石油樹脂の添加量
が3重量部未満では本発明の目的とする不透明化付与効
果が不足し、40重量部を越えると、成形時に押出ムラ
や延伸破断を生じ易く、生産性が極端に低下し、好まし
くない。The composition used in the present invention contains, in 100 parts by weight of polypropylene, 0.1 to 20 parts by weight of an inorganic filler powder and 3 to 40 parts by weight of a cyclopentadiene-based petroleum resin having a softening point (ring and ball method) of 160 ° C. or higher. . If the added amount of the inorganic filler is less than 0.1 part by weight, the light transmittance is large and the opacity is insufficient, and if it exceeds 20 parts by weight, problems such as clogging during film production, poor dispersion and stretch breakage are likely to occur, The obtained film is also unfavorable because the surface gloss and the pearly feeling are reduced. If the amount of the petroleum resin added is less than 3 parts by weight, the effect of imparting opacity, which is the object of the present invention, is insufficient, and if it exceeds 40 parts by weight, extrusion unevenness and stretch breakage tend to occur during molding, resulting in extremely high productivity. Is not preferable.
この無機充填剤と特定のシクロペンタジエン系石油樹脂
を特定の範囲で併用添加した組成物を延伸加工する事に
よって、きわめて優れた不透明で表面光沢の高い延伸成
形物が得られるのであり、特に好ましくは、ポリプロピ
レン100重量部に対し、平均粒径が10μ以下の炭酸
カルシウムまたはタルクを1〜10重量部と軟化点17
0〜200℃の水素化シクロペンタジエン系石油樹脂5
〜30重量部を添加した組成物、または平均粒径10μ
以下のシリカまたはゼオライトを0.1〜2重量部と軟
化点170〜200℃の水素化シクロペンタジエン系石
油樹脂5〜30重量部を添加した組成物を用いて同時な
いし逐次二軸延伸したもの又はこれらの併用形が特に好
ましい。By stretching the composition in which the inorganic filler and a specific cyclopentadiene-based petroleum resin are added together in a specific range, a stretched product having extremely excellent opacity and high surface gloss can be obtained, and particularly preferably. , 1 to 10 parts by weight of calcium carbonate or talc having an average particle size of 10 μ or less, and a softening point of 17 per 100 parts by weight of polypropylene.
Hydrogenated cyclopentadiene-based petroleum resin at 0 to 200 ° C 5
~ 30 parts by weight added composition, or average particle size 10μ
The following silica or zeolite is biaxially stretched simultaneously or sequentially using a composition to which 0.1 to 2 parts by weight and 5 to 30 parts by weight of a hydrogenated cyclopentadiene-based petroleum resin having a softening point of 170 to 200 ° C. are added, or A combination of these is particularly preferable.
本発明で用いるポリプロピレンと無機充填剤およびシク
ロペンタジエン系石油樹脂との組成物中には、必要に応
じて、ポリプロピレンに添加する事が公知な各種添加
剤、例えば公知のフェノール系ないしリン系ないしチオ
エーテル系等の加工安定剤・酸化防止剤、高級脂肪酸の
金属塩ないし脂肪酸アミド系等の滑剤・スリップ剤、帯
電防止剤、顔料及び各種ポリマー類等を配合してもよ
い。In the composition of the polypropylene used in the present invention and the inorganic filler and the cyclopentadiene-based petroleum resin, if necessary, various additives known to be added to polypropylene, such as known phenol-based or phosphorus-based or thioether A processing stabilizer / antioxidant such as a system, a lubricant / slip agent such as a metal salt of a higher fatty acid or a fatty acid amide, an antistatic agent, a pigment and various polymers may be added.
この組成物は、所定の配合物を通常のブレンダーまたは
ミキサー等で混合する事によって容易に得る事が出来る
が、押出機、バンバリーミキサー等を用いて結晶性ポリ
プロピレンの結晶融点及び該シクロペンタジエン系樹脂
の軟化点より10℃以上高い温度で溶融混合しペレット
状の組成物とするのが使用上特に好ましい。また、ポリ
プロピレンまたは他の樹脂に対し、無機充填剤または/
および該石油樹脂に多量に添加し、各々単独または併用
系でマスターバッチ化した後、ポリプロピレンと配合し
た混合組成物とするのも有用である。This composition can be easily obtained by mixing a predetermined blend with an ordinary blender, a mixer or the like, and the crystalline melting point of the crystalline polypropylene and the cyclopentadiene-based resin using an extruder, a Banbury mixer or the like. From the viewpoint of use, it is particularly preferable that the composition is pelletized by melt-mixing at a temperature higher than the softening point by 10 ° C. Also, for polypropylene or other resins, an inorganic filler or /
It is also useful to add a large amount to the petroleum resin, masterbatch each of them alone or in combination, and prepare a mixed composition with polypropylene.
こうして得られた組成物は、溶融押出機にて未延伸原反
を作成した後、公知の方法で一軸ないし二軸延伸する事
によって、フィルム、シート、ヤーン、フィラメント、
中空容器等の本発明の目的とする不透明化した延伸成形
物が得られる。この場合溶融押出は、組成物中の結晶性
ポリプロピレンの結晶融点及び該石油樹脂の軟化点の双
方より10℃以上高い温度で行うのが好ましく、押出さ
れた溶融樹脂を急冷して未延伸原反を成形し、この原反
を一軸ないし二軸延伸する。この延伸の方法は、ロール
延伸、オーブン延伸、熱板延伸等の公知の一軸延伸法な
いしチューブラー延伸、テンター法延伸等の同時ないし
逐次二軸延伸等の公知の方法のいずれでも良いが、その
延伸時の原反温度が用いる組成物中の該結晶性ポリプロ
ピレン及び該石油樹脂の軟化点より低い温度にする事が
必要であり、この条件を選択する事によって、全光線透
過率が50%以下で、かつ、密度が0.8g/cm3以下の
不透明化した延伸成形物を容易に得る事が出来る。The composition thus obtained, after forming an unstretched raw fabric with a melt extruder, by uniaxially or biaxially stretched by a known method, a film, a sheet, a yarn, a filament,
An opaque stretch-molded article intended for the present invention such as a hollow container can be obtained. In this case, the melt extrusion is preferably performed at a temperature higher than the crystal melting point of the crystalline polypropylene in the composition and the softening point of the petroleum resin by 10 ° C. or more. Is formed, and this original fabric is uniaxially or biaxially stretched. This stretching method may be any known method such as roll stretching, oven stretching, hot plate stretching or the like known uniaxial stretching method or tubular stretching, tenter method stretching or the like simultaneous or sequential biaxial stretching, etc., It is necessary to set the raw fabric temperature at the time of stretching to a temperature lower than the softening points of the crystalline polypropylene and the petroleum resin in the composition to be used. By selecting this condition, the total light transmittance is 50% or less. It is also possible to easily obtain an opaque stretched molded product having a density of 0.8 g / cm 3 or less.
なお、オーブン内での延伸等では熱風温度はポリプロピ
レンの融点以上に設定する事もあるが、ポリプロピレン
を融点以上で延伸・配向させる事は不可能であり、この
場合は、熱伝導と延伸原反の厚みと通過速度との関係
で、延伸原反の実温度は融点に達していない為であり、
本発明においては、この延伸原反の実温度を延伸温度と
言う。In the case of stretching in an oven, the hot air temperature may be set above the melting point of polypropylene, but it is not possible to stretch and orient polypropylene above the melting point. This is because the actual temperature of the drawn raw fabric has not reached the melting point due to the relationship between the thickness of the
In the present invention, the actual temperature of the original stretched fabric is referred to as the stretching temperature.
該組成物に用いるポリプロピレンの融点未満、該石油樹
脂の軟化点以下の温度で少なくとも一方向に2倍以上延
伸する事によって本発明の目的とする延伸成形物が得ら
れるが、面積で4倍以上の延伸が好ましく、面積倍率が
10〜60倍前後の高倍率延伸される同時ないし逐次二
軸延伸が特に好ましい。A stretched molded article aimed at by the present invention can be obtained by stretching at least 2 times in at least one direction at a temperature lower than the melting point of polypropylene used in the composition and at a temperature not higher than the softening point of the petroleum resin, but the area is 4 times or more. Is preferable, and simultaneous or sequential biaxial stretching in which high-area stretching having an area ratio of about 10 to 60 times is particularly preferable.
また、本発明の組成物を芯層とし、その延伸前または延
伸後に片面ないし両面にポリプロピレン系樹脂を主成分
とする層を形成し、その芯層のみを不透明化した積層体
も本発明は包含する。The present invention also includes a laminate in which the composition of the present invention is used as a core layer, and a layer containing a polypropylene-based resin as a main component is formed on one or both surfaces before or after the stretching, and only the core layer is opaque. To do.
本発明で用いる組成物を、延伸せずに成形して得られる
未延伸成形物では白濁した半透明成形物しか得られず、
密度はポリプロピレン単独よりも大きくなるので、本発
明の目的とする成形物は得られず、その外観、密度等か
ら容易に区分出来る。The composition used in the present invention, in the unstretched molded product obtained by molding without stretching, only a white translucent molded product is obtained,
Since the density is higher than that of polypropylene alone, the molded article aimed at by the present invention cannot be obtained, and it can be easily classified according to its appearance, density and the like.
本発明で得られる延伸成形物は、その全光線透過率が5
0%以下で、かつ、その密度が0.8g/cm3以下である
事が特徴であり、全光線透過率が50%を越えたもので
は不透明感が不足し、密度が0.8g/cm3を越えたもの
では内部発泡が不足し、不透明感、パール感のある延伸
成形品が得られない。全光線透過率が40%以下、密度
が0.75g/cm3以下の延伸成形品が不透明感・遮光性
およびパール光沢に優れ、特に好ましい。The stretched molded product obtained in the present invention has a total light transmittance of 5
The characteristic is that the density is 0% or less and the density is 0.8 g / cm 3 or less. If the total light transmittance exceeds 50%, the opacity is insufficient and the density is 0.8 g / cm 3. If it exceeds 3 , the internal foaming will be insufficient and an opaque and pearly stretch-molded product cannot be obtained. Stretch-molded products having a total light transmittance of 40% or less and a density of 0.75 g / cm 3 or less are particularly preferable because they are excellent in opacity, light-shielding property and pearl luster.
本発明で得られた延伸成形物には、必要に応じて空気、
酸素、窒素等の雰囲気下でコロナ処理、プラズマ処理等
の表面処理を施す事も出来る。The stretch-molded product obtained in the present invention, if necessary, air,
Surface treatment such as corona treatment and plasma treatment can be performed in an atmosphere of oxygen, nitrogen and the like.
以下、実施例、比較例によって本発明を更に具体的に説
明するが、本発明はこれらの実施例により制約されるも
のではない。なお、以下の実施例・比較例で用いた特性
地の評価方法は以下の方法で行った。Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples. The method for evaluating the characteristic ground used in the following examples and comparative examples was as follows.
(1).軟化点(環球法): JIS 2207による。(単位;℃) (2).ヨウ素価; JIS K0070−1966による。(1). Softening point (ring and ball method): According to JIS 2207. (Unit: ° C) (2). Iodine value; According to JIS K0070-1966.
試料100g中の不飽和成分に付加されるヨウ素のg数
をいう。It refers to the number of grams of iodine added to unsaturated components in 100 g of a sample.
(3).密 度: 成形物1m2当たりの重量を測定し、1cm2当たりに換算
し、厚さcmで除した値。(3). Density: A value obtained by measuring the weight per 1 m 2 of the molded product, converting it per 1 cm 2 , and dividing by the thickness cm.
(単位;g/cm3) (4).全光線透過率: JIS K−6714による。(Unit: g / cm 3 ) (4). Total light transmittance: According to JIS K-6714.
(5).ヘイズ(Haze): ASTM D1003による。(5). Haze: According to ASTM D1003.
(6).MFR(メルトフローレート): JIS K7210−1776の試験条件14(230
℃,2.16kgf)による。(単位;g/10mi
n.) (7).結晶融点(Tm): 走査型差動熱量計(略称;DSC)を用いて、約10mg
の試料をセットし、昇温速度20℃/分にて室温より測
定し、結晶の融解に伴う吸熱カーブを測定し、融解に伴
う吸熱カーブのピーク温度をTm(単位;℃)とした。
このとき、融解ピークが複数観察される場合は最大ピー
ク面積を有するものをTmとする。(6) .MFR (melt flow rate): JIS K7210-1776 test condition 14 (230
C., 2.16 kgf). (Unit: g / 10mi
n. (7). Crystal melting point (Tm): About 10 mg using a scanning differential calorimeter (abbreviation: DSC)
The sample was set and measured at room temperature at a temperature rising rate of 20 ° C./minute to measure the endothermic curve associated with melting of the crystal. The peak temperature of the endothermic curve associated with melting was defined as Tm (unit: ° C).
At this time, when a plurality of melting peaks are observed, the one having the maximum peak area is defined as Tm.
(実施例1〜8、比較例1〜4) MFR1.5、Tm163℃、n−ヘプタンに不溶性の
部分を94重量%含有する結晶性ポリプロピレン粉末1
00重量部に対し、フェノール系酸化防止剤BHT0.
1重量部、ステアリン酸カルシウム0.1重量部及び第
1表に示す無機充填剤および/または水素化シクロペン
タジエン系石油樹脂を所定量添加し、ヘンシェルミキサ
ーで混合した後、押出機を通して240℃で溶融混合
し、冷却・カットしてペレット状の組成物を得た。得ら
れた組成物をそれぞれ直径40mmの押出機及び30cm幅
のTダイを用いて260℃の温度で溶融押出し、45℃
に保った鏡面冷却ロールで急冷して厚さ1.2mmの未延
伸原反シートを得た。次に、この原反シートを正方形に
切断し、パンタグラフ型二軸延伸機を用いて155℃の
温度で70秒間予熱した後、同温度でタテ・ヨコ同時2
方向におのおの5.2倍延伸し、同温度で15秒間緊張
下で熱処理して13種類の二軸延伸フィルムを得た。得
られたフィルムの特性値を第1表に併記した。(Examples 1 to 8 and Comparative Examples 1 to 4) Crystalline polypropylene powder 1 containing MFR1.5, Tm of 163 ° C., and 94 wt% of an insoluble portion in n-heptane.
To 100 parts by weight of phenolic antioxidant BHT0.
1 part by weight, 0.1 part by weight of calcium stearate, and a predetermined amount of the inorganic filler and / or hydrogenated cyclopentadiene-based petroleum resin shown in Table 1 were added, mixed with a Henschel mixer, and then melted at 240 ° C. through an extruder. The mixture was mixed, cooled and cut to obtain a pelletized composition. Each of the obtained compositions was melt extruded at a temperature of 260 ° C. using an extruder having a diameter of 40 mm and a T-die having a width of 30 cm, and then 45 ° C.
It was rapidly cooled with a mirror-like cooling roll kept at the above temperature to obtain an unstretched raw sheet having a thickness of 1.2 mm. Next, this raw sheet is cut into squares, preheated at a temperature of 155 ° C. for 70 seconds using a pantograph type biaxial stretching machine, and then vertically and horizontally simultaneously 2
The film was stretched by 5.2 times in each direction and heat-treated under tension at the same temperature for 15 seconds to obtain 13 kinds of biaxially stretched films. The characteristic values of the obtained film are also shown in Table 1.
なお、該シクロペンタジエン系石油樹脂は、ナフサのス
チームクラッキングにより得られるシクロペンタジエン
あるいはジシクロペンタジエン類を、通常公知の方法で
重合時間、温度及び圧力を調整しつつ重合して得た。更
に、水素化はニッケル系触媒を用いて、250℃、80
kg/cm2の水素圧下で行って得たものを使用した。The cyclopentadiene-based petroleum resin was obtained by polymerizing cyclopentadiene or dicyclopentadiene obtained by steam cracking of naphtha by a commonly known method while adjusting the polymerization time, temperature and pressure. Furthermore, hydrogenation is performed at 250 ° C. and 80 ° C. using a nickel-based catalyst.
The one obtained under the hydrogen pressure of kg / cm 2 was used.
第1表から明らかなごとく、本発明に関わる無機充填剤
と該石油樹脂を特定の範囲内で添加した組成物を用いた
実施例1〜8のフィルムは、不透明度が高く(ヘイズが
大きく、光線透過率が小さい)、光沢度も高いが無機充
填剤のみを添加した比較例2のフィルムは不透明度が不
足(ヘイズが小さく、光線透過率が大きい)し、光沢度
も低く、該石油樹脂のみを添加した比較例4も全光線透
過率が高く、不透明度が不足している。As is clear from Table 1, the films of Examples 1 to 8 using the composition in which the inorganic filler according to the present invention and the petroleum resin are added within a specific range have high opacity (large haze, The film of Comparative Example 2 in which the light transmittance is small) and the glossiness is high but only the inorganic filler is added has insufficient opacity (small haze, high light transmittance), low glossiness, and the petroleum resin In Comparative Example 4 in which only the additive is added, the total light transmittance is also high and the opacity is insufficient.
又、比較例3から明らかなように、シクロペンタジエン
系石油樹脂と無機充填剤を併用添加した組成物を用いて
もシクロペンタジエン系樹脂の軟化点が本発明の範囲に
達しないと全光線透過率が高く、無機充填剤のみで、か
つ、その添加量も少ないもの(比較例2)よりも不透明
感が不足している事がわかる。Further, as is clear from Comparative Example 3, even if a composition in which a cyclopentadiene-based petroleum resin and an inorganic filler are added together is used and the softening point of the cyclopentadiene-based resin does not reach the range of the present invention, the total light transmittance is It is found that the opacity is less than that of the inorganic filler alone (Comparative Example 2) in which the amount of the inorganic filler is small and the amount thereof is small.
(比較例5) 実施例1で用いた組成物を、口径65mmφの単軸押出機
及び有効幅60mmのTダイを用いて260℃で溶融押出
し、25℃に保った直径400mmの粗面冷却ロールを用
いて冷却し、30m/min の速度で巻取り、幅400mm、
厚さ30μの未延伸フィルムを得た。得られた未延伸フ
ィルムは、密度0.90g/cm3、ヘイズ8.5%、全光
線透過率84%で、若干白濁感はあるがフィルムを通し
て物体を見る事の出来る透明タイプのフィルムであり、
未延伸フィルムの場合は、不透明化出来ない事がわか
る。 Comparative Example 5 The composition used in Example 1 was melt-extruded at 260 ° C. using a single-screw extruder having a diameter of 65 mmφ and a T-die having an effective width of 60 mm, and a rough surface cooling roll having a diameter of 400 mm kept at 25 ° C. Is cooled with a coil, and wound at a speed of 30 m / min, a width of 400 mm,
An unstretched film having a thickness of 30 μ was obtained. The obtained unstretched film was a transparent type film having a density of 0.90 g / cm 3 , a haze of 8.5%, and a total light transmittance of 84%, although there was a slight cloudiness, but an object could be seen through the film. ,
It can be seen that the unstretched film cannot be made opaque.
(実施例9) MFR2.0、Tm158℃、エチレン含有量0.4重
量%の結晶エチレン・プロピレンランダム共重合体に対
し、フェノール系酸化防止剤Irganox1010
(チバガイギー社製)0.2重量部、BHT0.1重量
部、ステアリン酸カルシウム0.15重量部、無機充填
剤として平均粒径3μのシリカ0.4重量部、軟化点
(環球法)172℃、分子量(GPC法)1542、シ
クロペンタジエン成分を約60重量%含有する水素化シ
クロペンタジエン系石油樹脂25重量部を配合し250
℃で溶融混練し、ペレット化した組成物とした。得られ
た組成物を実施例1と同様に260℃で溶融押出し、4
0℃の冷却ロールで急冷して厚み1.2mmの未延伸原反
を得た。得られた原反をパンタグラフ型二軸延伸装置を
用いて153℃の温度で60秒間予熱した後、原反シー
トの流れ(縦)方向に4.2倍延伸した後、直ちにその
直交(横)方向に9倍延伸し、同温度で両方向に3%弛
緩しつつ熱処理して厚み約40μの逐次二軸延伸フィル
ムを得た。Example 9 Phenolic antioxidant Irganox 1010 was added to a crystalline ethylene / propylene random copolymer having an MFR of 2.0, a Tm of 158 ° C. and an ethylene content of 0.4% by weight.
(Manufactured by Ciba-Geigy) 0.2 parts by weight, BHT 0.1 parts by weight, calcium stearate 0.15 parts by weight, 0.4 parts by weight of silica having an average particle size of 3 μ as an inorganic filler, softening point (ring and ball method) 172 ° C., 250 parts by weight of a hydrogenated cyclopentadiene-based petroleum resin containing a molecular weight (GPC method) of 1542 and a cyclopentadiene component of about 60% by weight was added to 250
The composition was melt-kneaded at ℃ and pelletized. The resulting composition was melt extruded at 260 ° C. as in Example 1 and 4
It was rapidly cooled with a 0 ° C. cooling roll to obtain an unstretched original fabric having a thickness of 1.2 mm. The obtained raw fabric was preheated at a temperature of 153 ° C. for 60 seconds using a pantograph-type biaxial stretching device, and then stretched 4.2 times in the flow (longitudinal) direction of the raw fabric, and then immediately orthogonal (transverse). The film was stretched 9 times in the direction and heat-treated at the same temperature while being relaxed by 3% in both directions to obtain a sequentially biaxially stretched film having a thickness of about 40 μm.
得られた二軸延伸フィルムは、密度0.61g/cm3、ヘ
イズ94%、全光線透過率22%及び光沢度55%と不
透明でパール光沢を有する美麗なフィルムであった。The obtained biaxially stretched film was a beautiful film having an opaque and pearly luster with a density of 0.61 g / cm 3 , a haze of 94%, a total light transmittance of 22% and a gloss of 55%.
(発明の効果) 従来公知の方法に比して、本発明は不透明延伸成形物が
きわめて生産性が高く、かつ、低コストで得る事が出
来、得られた成形品は、その不透明感、遮光性、軽量性
および独特のパール光沢を生かして一般包装材料、装飾
材料、梱包材料、織糸等の用途に広く実用出来る。(Effects of the Invention) Compared with conventionally known methods, the present invention can obtain an opaque stretched molded article with extremely high productivity and at low cost. It can be widely used for general packaging materials, decoration materials, packaging materials, woven yarn, etc. by taking advantage of its properties, light weight and unique pearl luster.
Claims (6)
し、無機充填剤粉末0.1〜20重量部および軟化点
(環球法)160℃以上のシクロペンタジエン系石油樹
脂3〜40重量部を配合した組成物からなり、微細な空
洞を多数有してその全光線透過率が50%以下、密度が
0.8g/cm3以下である不透明化した延伸成形物。1. A composition in which 0.1 to 20 parts by weight of an inorganic filler powder and 3 to 40 parts by weight of a cyclopentadiene-based petroleum resin having a softening point (ring and ball method) of 160 ° C. or higher are mixed with 100 parts by weight of crystalline polypropylene. An opaque stretch-molded product which is composed of a plurality of fine voids and has a total light transmittance of 50% or less and a density of 0.8 g / cm 3 or less.
し、無機充填剤粉末0.1〜20重量部および軟化点
(環球法)160℃以上の水素化シクロペンタジエン系
石油樹脂3〜40重量部を配合した組成物を、該結晶性
ポリプロピレンの結晶融点及び該石油樹脂の軟化点より
10℃以上高い温度で溶融押出し、冷却して未延伸原反
を作製した後、該結晶性ポリプロピレンの融点及び該石
油樹脂の軟化点より低い温度で、少なくとも一方向に2
倍以上延伸し、微細な空洞を多数発生させることを特徴
とする不透明化した延伸成形物の製造方法。2. An inorganic filler powder of 0.1 to 20 parts by weight and a softening point (ring and ball method) of 3 to 40 parts by weight of a hydrogenated cyclopentadiene-based petroleum resin having a softening point (ring and ball method) of 160 ° C. or more per 100 parts by weight of crystalline polypropylene. The composition prepared above is melt-extruded at a temperature higher than the crystalline melting point of the crystalline polypropylene and the softening point of the petroleum resin by 10 ° C. or more and cooled to prepare an unstretched raw material, and then the melting point of the crystalline polypropylene and the petroleum 2 at least in one direction at temperatures below the softening point of the resin
A method for producing an opaque stretched molded article, which comprises stretching a number of times to generate a large number of fine voids.
含有する石油樹脂を水素化して得られた軟化点(環球
法)170〜200℃、ヨウ素価20以下の水素化シク
ロペンタジエン系石油樹脂を用いた請求項1記載の不透
明化した延伸成形物。3. A hydrogenated cyclopentadiene-based petroleum resin having a softening point (ring and ball method) of 170 to 200 ° C. and an iodine value of 20 or less obtained by hydrogenating a petroleum resin containing 50% by weight or more of a cyclopentadiene component is used. The opaque stretch-molded article according to claim 1.
含有する石油樹脂を水素化して得られた軟化点(環球
法)170〜200℃、ヨウ素価20以下の水素化シク
ロペンタジエン系石油樹脂を用いることを特徴とする請
求項2記載の不透明化した延伸成形物の製造方法。4. A hydrogenated cyclopentadiene-based petroleum resin having a softening point (ring and ball method) of 170 to 200 ° C. and an iodine value of 20 or less obtained by hydrogenating a petroleum resin containing 50% by weight or more of a cyclopentadiene component. The method for producing an opaque stretched molded article according to claim 2.
炭酸カルシウムまたは/およびタルクを1〜10重量部
配合した組成物を用いることを特徴とする請求項2記載
の不透明化した延伸成形物の製造方法。5. An opaque stretch-molded article according to claim 2, wherein a composition containing 1 to 10 parts by weight of calcium carbonate or / and talc having an average particle size of 10 μm or less is used as the inorganic filler. Manufacturing method.
シリカまたは/および珪酸塩0.1〜2.0重量部を配
合した組成物を用いることを特徴とする請求項2記載の
不透明化した延伸成形物の製造方法。6. The opacifying agent according to claim 2, wherein a composition containing 0.1 to 2.0 parts by weight of silica or / and a silicate having an average particle diameter of 10 μm or less is used as the inorganic filler. Of producing the stretched molded product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001053A JPH0649790B2 (en) | 1990-01-09 | 1990-01-09 | Opaque stretched molded article and method for producing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001053A JPH0649790B2 (en) | 1990-01-09 | 1990-01-09 | Opaque stretched molded article and method for producing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03207730A JPH03207730A (en) | 1991-09-11 |
| JPH0649790B2 true JPH0649790B2 (en) | 1994-06-29 |
Family
ID=11490805
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001053A Expired - Fee Related JPH0649790B2 (en) | 1990-01-09 | 1990-01-09 | Opaque stretched molded article and method for producing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0649790B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2514549B2 (en) * | 1992-09-16 | 1996-07-10 | チッソ株式会社 | Laminated polypropylene sheet |
| JP2519877Y2 (en) * | 1992-10-02 | 1996-12-11 | チッソ株式会社 | Watermarked laminated polypropylene sheet |
| JP2504438Y2 (en) * | 1993-03-04 | 1996-07-10 | チッソ株式会社 | Partially laminated polypropylene sheet |
| JP2504445Y2 (en) * | 1993-05-06 | 1996-07-10 | チッソ株式会社 | Laminated polypropylene sheet molding |
| JP4659163B2 (en) * | 1999-06-15 | 2011-03-30 | 凸版印刷株式会社 | Aluminum transfer deposition thin leaf |
-
1990
- 1990-01-09 JP JP2001053A patent/JPH0649790B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03207730A (en) | 1991-09-11 |
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